EP2398609B2 - Casting process of aluminium alloys - Google Patents

Casting process of aluminium alloys Download PDF

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Publication number
EP2398609B2
EP2398609B2 EP10707100.3A EP10707100A EP2398609B2 EP 2398609 B2 EP2398609 B2 EP 2398609B2 EP 10707100 A EP10707100 A EP 10707100A EP 2398609 B2 EP2398609 B2 EP 2398609B2
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Prior art keywords
casting
gas
process according
dried gas
aluminum alloy
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German (de)
French (fr)
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EP2398609B1 (en
EP2398609A1 (en
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Guillaume Bes
Robert Rey-Flandrin
Olivier Ribaud
Stéphane VERNEDE
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Constellium Issoire SAS
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Constellium Issoire SAS
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D21/00Casting non-ferrous metals or metallic compounds so far as their metallurgical properties are of importance for the casting procedure; Selection of compositions therefor
    • B22D21/02Casting exceedingly oxidisable non-ferrous metals, e.g. in inert atmosphere
    • B22D21/04Casting aluminium or magnesium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/001Continuous casting of metals, i.e. casting in indefinite lengths of specific alloys
    • B22D11/003Aluminium alloys
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/04Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/10Supplying or treating molten metal
    • B22D11/11Treating the molten metal
    • B22D11/116Refining the metal
    • B22D11/117Refining the metal by treating with gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/12Accessories for subsequent treating or working cast stock in situ
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D21/00Casting non-ferrous metals or metallic compounds so far as their metallurgical properties are of importance for the casting procedure; Selection of compositions therefor
    • B22D21/002Castings of light metals
    • B22D21/007Castings of light metals with low melting point, e.g. Al 659 degrees C, Mg 650 degrees C

Definitions

  • the invention relates to the casting of aluminum alloys, in particular the casting of alloys containing magnesium and/or lithium which are sensitive to oxidation.
  • beryllium has a certain toxicity which has notably led to its elimination in aluminum alloys used as food packaging. Calcium can cause edge cracks during hot rolling. It has also been proposed to protect the surface of the liquid metal by various devices.
  • the patent US 4,582,118 proposes using a non-reactive and non-combustible atmosphere, such as for example an atmosphere of argon, helium, neon, or krypton or even nitrogen or carbon dioxide, for the casting of aluminum alloys- lithium. The implementation of such methods is however very expensive.
  • the patent application EP 0 109 170 A1 describes the use of a baffle on the periphery of the casting loom to sweep the liquid metal surface with an inert gas (usually nitrogen and/or argon with or without chlorine or other halogen).
  • an inert gas usually nitrogen and/or argon with or without chlorine or other halogen.
  • carbon dioxide or flue gases to limit oxidation is also known from CN Cochran, DL Belitskus and DL Kinosz, Metallurgical Transcations B, Volume 8B, 1977, pages 323-331 .
  • the patent application EP 1 964 628 A1 describes a method for producing aluminum ingots in which at least one process step is carried out under an atmosphere containing a fluorinated gas.
  • the patent US 5,415,220 describes the use of molten salts of lithium chloride and potassium chloride to protect the surface of aluminium-lithium alloys during casting.
  • the use of molten salts has the disadvantage of the risk of contamination of the liquid metal with impurities as well as the difficulty of implementation.
  • the patent US 7,267,158 describes the forced addition of a moist gas, containing more than 0.005 kg/m 3 of water, to the surface of the molten metal so as to improve the surface quality of the cast ingots.
  • this process has the disadvantage of bringing the steam and the liquid aluminum into contact despite the dangers of explosion linked to the contact of the water and the liquid aluminum.
  • the document US-A-2005/000677 discloses a method of casting an aluminum alloy containing at least 0.1% by weight of Mg in which a liquid surface of said alloy is contacted during solidification with a dry gas comprising at least about 2% by volume of oxygen and whose water partial pressure has a dew point of 0°C.
  • the problem posed is to find a casting process suitable for the most oxidizable aluminum alloys, in particular aluminum alloys containing magnesium and/or lithium, which does not have these drawbacks and makes it possible to obtain cast ingots free from surface defects and pollution, in complete safety.
  • a first object of the invention is a method of casting an aluminum alloy containing at least approximately 0.1% Mg and/or at least approximately 0.1% Li according to claim 1.
  • the designation of the alloys follows the rules of The Aluminum Association, known to those skilled in the art.
  • the chemical composition of standardized aluminum alloys is defined for example in standard EN 573-3. Unless otherwise stated, the definitions of the European standard EN 12258-1 apply.
  • the term “casting installation” is used here to refer to all the devices making it possible to transform a metal in any form into a semi-finished product in raw form by passing through the liquid phase.
  • a casting installation can include many devices such as one or more furnaces necessary for melting the metal and/or maintaining it at temperature and/or for preparing the liquid metal and adjusting the composition, one or several tanks (or “pockets") intended to carry out a treatment for the elimination of impurities dissolved and/or suspended in the liquid metal, this treatment possibly consisting in filtering the liquid metal on a filter medium in a "filtration pocket” or introducing a so-called “treatment” gas into the bath, which may be inert or reactive, in a “degassing ladle", a device for solidifying the liquid metal (or “casting machine"), for example by vertical semi-continuous casting by direct cooling, horizontal casting, continuous wire casting, continuous strip casting between rolls, continuous strip casting between caterpillars, which may include devices such as a mold (or “mold”) ), a liquid metal supply device (or “nozzle”) a cooling system, these various furnaces, tanks and solidification devices being interconnected by channels called “chutes” in which the liquid metal can be transported.
  • devices such
  • the present inventors have found that, when brought into contact with a dry gas comprising at least approximately 2% by volume of oxygen and whose water partial pressure is less than approximately 150 Pa, a surface of liquid aluminum s oxidizes little, which makes it possible to make castings free from unacceptable surface defects.
  • a surface of liquid aluminum s oxidizes little, which makes it possible to make castings free from unacceptable surface defects.
  • This result is surprising because it is commonly accepted that, on the contrary, the humidity contained in the air makes it possible to limit the oxidation of aluminum alloys in the liquid state.
  • this surprising effect is implemented in a casting process.
  • the method according to the invention is useful for highly oxidizable aluminum alloys, containing at least approximately 0.1% of Mg and/or at least approximately 0.1% of Li.
  • the method according to the invention is particularly useful for alloys of families 2XXX, 3XXX, 5XXX, 6XXX, 7XXX or 8XXX, in particular when these alloys do not contain any deliberate addition of beryllium and/or calcium.
  • the process according to the invention is particularly advantageous for alloys containing less than 3 ppm of beryllium or even less than 1 ppm of beryllium and/or less than 15 ppm of calcium or even less than 5 ppm of calcium.
  • alloys for which the process according to the invention is particularly advantageous are, in the family of 2XXX alloys, the alloys AA2014, AA2017, AA2024, AA2024A, AA2027, AA2139, AA2050, AA2195, AA2196, AA2098, AA2198, AA2214 , AA2219, AA2524 in the 3XXX alloy family AA3003, AA3005, AA3104, AA3915 alloys in the 5XXX alloy family 7XXX alloys AA7010, AA7020, AA7040, AA7140, AA7050, AA7055, AA7056, AA7075, AA7449, AA7450, AA7475, AA7081, AA7085, AA7910, AA7975.
  • the dried gas must contain at least about 2% by volume of oxygen and have a water partial pressure of less than about 150 Pa, preferably less than 100 Pa and even more preferably less than 70 Pa. particularly advantageous invention, the partial water pressure is even less than 30 Pa, preferably less than 5 Pa and even more preferably less than 1 Pa.
  • the water partial pressure of a gas is also known as the vapor pressure.
  • the partial pressure of an ideal gas i in a mixture of ideal gases of total pressure P is defined as the pressure which would be exerted by the molecules of gas i if this gas alone occupied all the volume offered to the mixture.
  • the dew point of a gas is the temperature at which, while keeping current barometric conditions unchanged, the gas becomes saturated with water vapour.
  • a water partial pressure of 150 Pa corresponds to a dew point of -17.9°C and a quantity of water of 0.0013 kg/m 3 at this temperature.
  • a water partial pressure of 100 Pa corresponds to a dew point of -22.6°C and a quantity of water of 0.0009 kg/m 3 at this temperature.
  • a water partial pressure of 70 Pa corresponds to a dew point of -26.5°C and a quantity of water of 0.0006 kg/m 3 at this temperature.
  • the dried gas also advantageously comprises at least one gas selected from air, helium, argon, nitrogen, carbon dioxide, carbon monoxide, natural gas combustion products, methane, ethane, propane, natural gas, organic fluorinated compounds, organic chlorine compounds. Adding carbon dioxide to the dry gas can in some cases enhance the antioxidant effect.
  • the dry gas comprises between 1 and 10% by volume of CO 2
  • the CO 2 content of the dry gas is less than 1% by volume or even less than 0.1% by volume in another advantageous embodiment of the invention.
  • said dried gas is essentially air dried by any appropriate means to reach the desired water partial pressure.
  • the dried gas is brought into contact with a liquid surface of an aluminum alloy during most of the solidification of said alloy.
  • the bringing into contact of the gas with the surface is preferably carried out in such a way as to establish above this surface an atmosphere whose water content is substantially equal, generally different by less than 10% or 20%, to that of the dry gas, that is to say so as to avoid a significant diffusion of water vapor from the ambient air into said atmosphere.
  • this flow it is advantageous for this flow to be sufficient with respect to the liquid surface subjected to the dry flow so as to establish said atmosphere, if this flow is too low, the composition of said atmosphere may be influenced too much by the external atmosphere and its water content may no longer correspond to the desired content.
  • the liquid surface of the aluminum alloy brought into contact with the dried gas represents at least 10%, preferably at least 25% and even more preferably at least 50% of the total liquid surface of said aluminum alloy.
  • a liquid surface of the aluminum alloy is kept in contact with the dry gas during most of the solidification.
  • an increase in the flow rate of a flow of dry gas makes it possible in certain cases to make furrows disappear in the cast product.
  • the contact between the liquid surface and the dried gas can possibly be eliminated before the end of the casting, in particular when a zone is reached which will be cut off during the following operations.
  • a liquid surface of the aluminum alloy is kept in contact with the dry gas for at least 50% or even at least 90% of the solidification.
  • the present invention applies to various casting processes and preferably to a casting process chosen from among vertical semi-continuous casting by direct cooling, horizontal casting, continuous casting of wire, continuous casting of strips between rolls, continuous casting of strips between caterpillars (“belt caster”).
  • the semi-continuous process of vertical casting by direct cooling of aluminum alloys known to those skilled in the art in particular by its name in English "Direct Chill casting” or "DC casting”, is a preferred process in the context of the present invention.
  • an aluminum alloy is poured into an ingot mold having a false bottom by moving vertically and continuously the false bottom so as to maintain a substantially constant level of liquid metal during the solidification of the alloy, the solidified faces being cooled directly with water.
  • the figure 1 illustrates this process.
  • the aluminum alloy is fed through a conduit (4) into a mold (3) placed on a false bottom (21).
  • the aluminum alloy solidifies by direct cooling (5).
  • the solidifying aluminum alloy (1) has at least one solid surface (11, 12, 13) and at least one liquid state aluminum alloy surface which can be coated with oxides, which is called “liquid surface” in the present description (14, 15).
  • a descender (2) makes it possible to gradually lower the alloy during solidification so as to maintain the vertical position of the liquid aluminum surface (14, 15) substantially constant.
  • the method according to the invention is particularly advantageous for the casting of plates and billets by vertical semi-continuous casting by direct cooling.
  • the process according to the invention is particularly advantageous for the casting of plates of large dimensions, in particular with a section greater than 0.5 m 2 .
  • the device is fixed around a liquid metal injector so as to introduce the dried gas from the center of the liquid surface towards its periphery and/or from the periphery towards the center.
  • a device for the supply of gas in the case of semi-continuous vertical casting by direct cooling is illustrated by the figure 2 .
  • the dry gas is supplied by means of a device (6) fixed around the liquid metal injector (4) so that the flow of dry gas (7) is directed from the core of said liquid surface towards its periphery and/or from the periphery towards the core in the liquid metal injection zone.
  • the gas supply device can be fixed on a dam retaining the oxides (“dross dam”) which is positioned around the liquid metal injection zone.
  • the dry gas from the casting process according to the invention can also be used in other parts of a casting installation on a liquid surface of aluminum alloys containing at least about 0.1% Mg and/or at least about 0.1% Li, to minimize oxidation.
  • a casting installation includes several other devices in which liquid surfaces of aluminum alloy are in contact with the atmosphere.
  • the dried gas can advantageously be used to limit the oxidation of the liquid surface of alloys in a furnace, in particular melting or holding, in a treatment tank such as a filtration ladle or a degassing ladle or in a transfer channel such as a chute.
  • conditions for using the dried gas and/or an aluminum alloy composition similar to those of the process according to the invention are preferably used, in particular concerning the supply of the dried gas.
  • the dried gas is also used in at least one furnace, in particular melting or holding and/or in at least one treatment tank such as a filtration ladle or a degassing ladle and/or in at least one transfer channel such as a chute .
  • the products obtained by a process according to the invention and/or by a use according to the invention can optionally be wrought in particular by rolling, spinning and/or forging, so as to obtain in particular sheets and profiles.
  • the invention allows in particular the casting of the most oxidizable aluminum alloys, in particular aluminum alloys containing magnesium and/or lithium, without using additives such as beryllium and/or calcium and without using expensive device and/or gas while obtaining cast ingots free from surface defects and pollution, in complete safety.
  • the oxidation of the liquid metal was measured by thermogravimetric analysis.
  • a crucible containing the liquid metal is maintained at a controlled temperature.
  • This crucible contains approximately 5 kg of metal, for a diameter of 100 mm.
  • the significant size of these experiments which makes it possible to take macroscopic effects into account, may explain the differences with the experiments carried out on very small quantities often reported in the prior art.
  • the mass of the sample is weighed continuously. The weight gain is due to the oxidation of the liquid metal.
  • a diagram illustrating this experiment is presented on the figure 4 .
  • the dried gas (7) is brought to the surface of the liquid metal (14) by a metal tube (6) with an inside diameter of 4 mm, arranged obliquely with respect to this surface.
  • the balance (92) makes it possible to continuously measure the weight of the crucible (93) and of its contents in situ in the furnace (91).
  • the distance between the orifice of the metal tube and the surface of the liquid metal was 120 mm.
  • the air used can be dried until it reaches a water partial pressure of less than 70 Pa.
  • Three alloys were studied: the AA7449, AA2196 and AA5182 alloys. The conditions of the different runs are summarized in Table 1. In all runs, beryllium and calcium content were similar and less than 1 ppm and 10 ppm, respectively. Table 1.
  • thermobalance Trials alloy Gas flow (1/min) Gas Water partial pressure of the injected gas (Pa) 1 AA5182 7.9 Dry air ⁇ 70Pa 2 AA5182 0 Ambiant air > 600Pa 3 AA2196 7.9 Dry air ⁇ 70Pa 4 AA2196 0 Ambiant air > 600Pa 5 AA7449 4.1 Dry air ⁇ 70Pa 6 AA7449 3.8 Ambiant air > 600Pa 7 AA7449 0 Ambiant air > 600Pa 8 AA7449 4.1 Dry air 180Pa 9 AA7449 3.8 Dry air 600Pa
  • the figures 5 to 8 present the results obtained.
  • the figure 5 shows the results obtained with the AA7449 alloy. Significantly lower weight gains are obtained for test 5 for which a very dry air flow was carried out. Bringing a liquid surface into contact with dry air whose water partial pressure is still 600 Pa (dew point of -0.2°C, test 9) or even 180 Pa (dew point -15.6°C, test 8) do not significantly limit oxidation. Likewise, the ambient air does not make it possible to limit the oxidation with or without flow (tests 6 and 7), which excludes a purely mechanical effect linked to a flow of gas.
  • the figure 6 shows the results obtained with the AA5182 alloy. A significantly lower oxidation in the presence of a very dry air flow is also observed for this alloy.
  • the figure 7 shows the results obtained with the AA2196 alloy. Again, for this alloy, significantly lower oxidation is observed in the presence of a very dry air flow.
  • the figure 8a is a photograph of the surface obtained after the test in the case of test 7 (ambient air). A very significant oxidation is observed, leading to oxidation products in the characteristic form of dark colored cauliflower.
  • the figure 8b is a photograph of the surface obtained after the test in the case of test 5 (dry air). A uniform surface of light gray color corresponding to a thin oxide film is observed.
  • Plates of rectangular section 446 mm x 2160 mm in AA7449 alloy were cast vertically using a semi-continuous direct-chill casting (DC-cast) installation, using an AlTiC quench.
  • the length of the plates obtained was between 900 mm and 4000 mm.
  • the beryllium content of the alloy was less than 1 ppm and the calcium content was less than 15 ppm.
  • the picture 3 illustrates the gas supply device having been used to supply dry air during the casting of the plates.
  • the device consists of 4 tubes (611, 612, 621 and 622) regularly pierced with orifices (63) making it possible to inject the dried gas (7) onto the liquid surface of the aluminum alloy.
  • the tubes are connected by screw connections (9) to form a rectangle.
  • the tubes are supplied with gas by two of these screwed connections, by two pipes (81) and (82).
  • the dried gas was dry air with a water partial pressure of 60 Pa, containing in some cases 5% by volume of CO 2 .
  • Table 2 describes the conditions of the various tests carried out as well as the results obtained. Table 2. Casting test condition and results obtained. Test Cast length [mm] dry air flow [m 3 /h] (cast length) % CO2 of dry air flow comments 21 917 Any - Long ( ⁇ 200mm) and deep vertical furrows 22 2776 None (Startup) - Long ( ⁇ 200mm) and deep vertical furrows 22 (1150mm) 5% No furrow 23 3575 22 (Start) 0% A few short (-40 mm) and shallow vertical furrows 27 (1150mm) 0% A few short (-40 mm) and shallow vertical furrows 32 (2500mm) 0% No furrow

Description

Domaine de l'inventionField of the invention

L'invention concerne la coulée des alliages d'aluminium, notamment la coulée des alliages contenant du magnésium et / ou du lithium sensibles à l'oxydation.The invention relates to the casting of aluminum alloys, in particular the casting of alloys containing magnesium and/or lithium which are sensitive to oxidation.

Etat de la techniqueState of the art

L'oxydation des alliages d'aluminium à l'état liquide a des conséquences néfastes sur le procédé de fonderie. Dans les fours et les chenaux de transfert, l'oxydation du métal a tout d'abord pour résultat une perte nette de métal, appelée perte au feu. De plus, lors de la coulée, une oxydation trop importante du métal liquide engendre des défauts à la surface du lingot coulé qui nuisent à l'utilisation des produits. Ces problèmes sont particulièrement prononcés dans les alliages contenant du magnésium et / ou du lithium.
Un défaut principal est le sillon vertical qui est notamment généré par des plissements de la peau d'oxyde en surface du marais. Dans certains cas, et notamment lors de la coulée des alliages 7xxx, ce problème est particulièrement important car les sillons, surtout quand ils sont longs et profonds, initient facilement des fentes de surface. Les sillons et les fentes doivent généralement être éliminés avant la transformation des lingots obtenus lors de la coulée. On peut, par exemple, éliminer les défauts par usinage, ce qui peut être économiquement très défavorable tant par le coût de l'opération que par la perte significative de métal qui en résulte. Dans certains cas, la présence de fente rend le lingot inutilisable et il est nécessaire de le refondre.
The oxidation of aluminum alloys in the liquid state has harmful consequences on the foundry process. In furnaces and transfer channels, the oxidation of metal first results in a net loss of metal, called loss on ignition. In addition, during casting, excessive oxidation of the liquid metal generates defects on the surface of the cast ingot which are detrimental to the use of the products. These problems are particularly pronounced in alloys containing magnesium and/or lithium.
A main defect is the vertical furrow which is notably generated by folding of the oxide skin at the surface of the marsh. In some cases, and in particular when casting 7xxx alloys, this problem is particularly important because the grooves, especially when they are long and deep, easily initiate surface splits. The grooves and cracks must generally be eliminated before the processing of the ingots obtained during the casting. It is possible, for example, to eliminate the defects by machining, which can be economically very unfavorable both by the cost of the operation and by the significant loss of metal which results therefrom. In some cases, the presence of a crack makes the ingot unusable and it is necessary to remelt it.

Il est connu de longue date que l'ajout de certains éléments permet de limiter l'oxydation et d'améliorer la qualité de surface.
Dès 1943, le brevet US 2,336,512 décrivait l'addition de très faibles quantités béryllium à des alliages d'aluminium contenant du magnésium de façon à limiter l'oxydation de la surface de métal liquide.
La demande internationale WO 02/30822 décrit la substitution du béryllium par le calcium dans un but identique de limitation de l'oxydation.
It has long been known that the addition of certain elements makes it possible to limit oxidation and improve surface quality.
As early as 1943, the patent US 2,336,512 described the addition of very small amounts of beryllium to aluminum alloys containing magnesium in order to limit oxidation of the liquid metal surface.
The international request WO 02/30822 describes the substitution of beryllium by calcium for the same purpose of limiting oxidation.

L'ajout d'éléments d'additions peut cependant être la cause d'autres problèmes. Ainsi, le béryllium présente une certaine toxicité ce qui a notamment conduit à sa suppression dans les alliages d'aluminium utilisés en tant qu'emballages alimentaires. Le calcium peut quant à lui être à l'origine de fissures de rive lors du laminage à chaud.
On a également proposé de protéger la surface du métal liquide par différents artifices.
Le brevet US 4,582,118 propose d'utiliser une atmosphère non réactive et non combustible, telle que par exemple une atmosphère d'argon, d'hélium, de néon, ou de krypton ou encore d'azote ou de dioxyde de carbone, pour la coulée des alliages aluminium-lithium. La mise en oeuvre de tels procédés est cependant très coûteuse.
La demande de brevet EP 0 109 170 A1 décrit l'utilisation d'une chicane sur la périphérie du métier de coulée pour balayer la surface de métal liquide par un gaz inerte (habituellement de l'azote et/ou de l'argon avec ou sans chlore ou un autre halogène). Cependant la mise en oeuvre de ces gaz est délicate et augmente significativement le coût des opérations. L'utilisation de dioxyde de carbone ou de gaz de combustion pour limiter l'oxydation est également connue de C.N. Cochran, D.L. Belitskus et D.L. Kinosz, Metallurgical Transcations B, Volume 8B, 1977, pages 323-331 .
La demande de brevet EP 1 964 628 A1 décrit une méthode pour produire des lingots d'aluminium dans laquelle au moins une étape du procédé est conduite sous une atmosphère contenant un gaz fluoré. Cependant la mise en oeuvre de gaz fluorés est délicate et crée des risques importants vis-à-vis des personnes.
Le brevet US 5,415,220 décrit l'utilisation de sels fondus de chlorure de lithium et de chlorure de potassium pour protéger la surface d'alliages aluminium-lithium lors de la coulée. Cependant l'utilisation de sels fondus a pour inconvénient le risque de contamination du métal liquide en impuretés ainsi que la difficulté de mise en oeuvre.
Le brevet US 7,267,158 décrit l'addition forcée d'un gaz humide, contenant plus de 0,005 kg/m3 d'eau, à la surface du métal fondu de façon à améliorer la qualité de surface des lingots coulés. Ce procédé présente cependant l'inconvénient de mettre en contact la vapeur d'eau et l'aluminium liquide en dépit des dangers d'explosion liés au contact de l'eau et de l'aluminium liquide.
Par ailleurs, il est connu de la demande EP 0 216 393 A1 d'utiliser de l'air sec dans une poche de traitement de l'aluminium liquide pour éviter la pénétration d'hydrogène dans le métal fondu lorsqu'un gaz de traitement est injecté dans le métal liquide et provoque la rupture de la couche d'oxyde protégeant sa surface.
However, adding addition elements can cause other problems. Thus, beryllium has a certain toxicity which has notably led to its elimination in aluminum alloys used as food packaging. Calcium can cause edge cracks during hot rolling.
It has also been proposed to protect the surface of the liquid metal by various devices.
The patent US 4,582,118 proposes using a non-reactive and non-combustible atmosphere, such as for example an atmosphere of argon, helium, neon, or krypton or even nitrogen or carbon dioxide, for the casting of aluminum alloys- lithium. The implementation of such methods is however very expensive.
The patent application EP 0 109 170 A1 describes the use of a baffle on the periphery of the casting loom to sweep the liquid metal surface with an inert gas (usually nitrogen and/or argon with or without chlorine or other halogen). However, the use of these gases is tricky and significantly increases the cost of operations. The use of carbon dioxide or flue gases to limit oxidation is also known from CN Cochran, DL Belitskus and DL Kinosz, Metallurgical Transcations B, Volume 8B, 1977, pages 323-331 .
The patent application EP 1 964 628 A1 describes a method for producing aluminum ingots in which at least one process step is carried out under an atmosphere containing a fluorinated gas. However, the use of fluorinated gases is delicate and creates significant risks with respect to people.
The patent US 5,415,220 describes the use of molten salts of lithium chloride and potassium chloride to protect the surface of aluminium-lithium alloys during casting. However, the use of molten salts has the disadvantage of the risk of contamination of the liquid metal with impurities as well as the difficulty of implementation.
The patent US 7,267,158 describes the forced addition of a moist gas, containing more than 0.005 kg/m 3 of water, to the surface of the molten metal so as to improve the surface quality of the cast ingots. However, this process has the disadvantage of bringing the steam and the liquid aluminum into contact despite the dangers of explosion linked to the contact of the water and the liquid aluminum.
Furthermore, it is known from the application EP 0 216 393 A1 to use dry air in a liquid aluminum treatment ladle to prevent hydrogen from entering the molten metal when a treatment gas is injected into the liquid metal and causes the rupture of the layer of oxide protecting its surface.

Le document US-A-2005/000677 divulgue un procédé de coulée d'un alliage d'aluminium contenant au moins 0, 1 % en poids de Mg dans lequel on met en contact pendant la solidification une surface liquide dudit alliage avec un gaz asséché comprenant au moins environ 2% en volume d'oxygène et dont la pression partielle en eau présente un point de rosée de 0°C.The document US-A-2005/000677 discloses a method of casting an aluminum alloy containing at least 0.1% by weight of Mg in which a liquid surface of said alloy is contacted during solidification with a dry gas comprising at least about 2% by volume of oxygen and whose water partial pressure has a dew point of 0°C.

Le problème posé est de trouver un procédé de coulée adapté aux alliages d'aluminium les plus oxydables, en particulier les alliages d'aluminium contenant du magnésium et/ou du lithium, qui ne présente pas ces inconvénients et permette d'obtenir des lingots coulés exempts de défauts de surface et de pollutions, en toute sécurité.The problem posed is to find a casting process suitable for the most oxidizable aluminum alloys, in particular aluminum alloys containing magnesium and/or lithium, which does not have these drawbacks and makes it possible to obtain cast ingots free from surface defects and pollution, in complete safety.

Description de l'inventionDescription of the invention

Un premier objet de l'invention est un procédé de coulée d'un alliage d'aluminium contenant au moins environ 0,1% de Mg et/ou au moins environ 0,1% de Li selon la revendication 1.A first object of the invention is a method of casting an aluminum alloy containing at least approximately 0.1% Mg and/or at least approximately 0.1% Li according to claim 1.

Description des figuresDescription of figures

  • Figure 1 : schéma général d'une installation de coulée verticale semi-continue. Figure 1 : general diagram of a semi-continuous vertical casting installation.
  • Figure 2: schéma d'une installation de coulée verticale incluant un dispositif d'approvisionnement d'un flux de gaz asséché. Figure 2 : diagram of a vertical casting installation including a device for supplying a flow of dried gas.
  • Figure 3 : schéma d'un dispositif d'approvisionnement d'un flux de gaz asséché pour la coulée de plaques. Figure 3 : diagram of a device for supplying a flow of dry gas for the casting of plates.
  • Figure 4 : schéma de la thermo-balance utilisée dans l'exemple 1. Figure 4 : diagram of the thermo-balance used in example 1.
  • Figure 5 : évolution de la prise de poids avec le temps pour les expériences réalisées avec l'alliage 7449 dans l'exemple 1. Figure 5 : evolution of weight gain over time for the experiments carried out with the 7449 alloy in example 1.
  • Figure 6: géométrie évolution de la prise de poids avec le temps pour les expériences réalisées avec l'alliage AA5182 dans l'exemple 1. Figure 6 : geometry evolution of weight gain over time for the experiments carried out with the AA5182 alloy in example 1.
  • Figure 7 : évolution de la prise de poids avec le temps pour les expériences réalisées avec l'alliage AA2196 dans l'exemple 1. Picture 7 : evolution of weight gain over time for the experiments carried out with the AA2196 alloy in example 1.
  • Figure 8 : photographies des surfaces obtenues après les essais N° 7 (Fig. 8a) et N°5 (Fig. 8b) de l'exemple 1. Figure 8 : photographs of the surfaces obtained after tests No. 7 ( Fig. 8a ) and No. 5 ( Fig. 8b ) of example 1.
Description détaillée de l'inventionDetailed description of the invention

La désignation des alliages suit les règles de The Aluminum Association, connues de l'homme du métier. La composition chimique d'alliages d'aluminium normalisés est définie par exemple dans la norme EN 573-3.
Sauf mention contraire, les définitions de la norme européenne EN 12258-1 s'appliquent. On appelle ici « installation de coulée » l'ensemble des dispositifs permettant de transformer un métal sous forme quelconque en demi-produit de forme brute en passant par la phase liquide. Une installation de coulée peut comprendre de nombreux dispositifs tels que un ou plusieurs fours nécessaires à la fusion du métal et/ou à son maintien en température et/ou à des opérations de préparation du métal liquide et d'ajustement de la composition, une ou plusieurs cuves (ou « poches ») destinées à effectuer un traitement d'élimination des impuretés dissoutes et/ou en suspension dans le métal liquide, ce traitement pouvant consister à filtrer le métal liquide sur un média filtrant dans une « poche de filtration » ou à introduire dans le bain un gaz dit « de traitement » pouvant être inerte ou réactif dans une « poche de dégazage », un dispositif de solidification du métal liquide (ou « métier de coulée »), par exemple par coulée semi-continue verticale par refroidissement direct, coulée horizontale, coulée continue de fil, coulée continue de bandes entre cylindres, coulée continue de bandes entre chenilles, pouvant comprendre des dispositifs tels que un moule (ou « lingotière »), un dispositif d'approvisionnement du métal liquide (ou « busette ») un système de refroidissement, ces différents fours, cuves et dispositifs de solidification étant reliés entre eux par des chenaux appelés « goulottes » dans lesquels le métal liquide peut être transporté.
The designation of the alloys follows the rules of The Aluminum Association, known to those skilled in the art. The chemical composition of standardized aluminum alloys is defined for example in standard EN 573-3.
Unless otherwise stated, the definitions of the European standard EN 12258-1 apply. The term “casting installation” is used here to refer to all the devices making it possible to transform a metal in any form into a semi-finished product in raw form by passing through the liquid phase. A casting installation can include many devices such as one or more furnaces necessary for melting the metal and/or maintaining it at temperature and/or for preparing the liquid metal and adjusting the composition, one or several tanks (or "pockets") intended to carry out a treatment for the elimination of impurities dissolved and/or suspended in the liquid metal, this treatment possibly consisting in filtering the liquid metal on a filter medium in a "filtration pocket" or introducing a so-called "treatment" gas into the bath, which may be inert or reactive, in a "degassing ladle", a device for solidifying the liquid metal (or "casting machine"), for example by vertical semi-continuous casting by direct cooling, horizontal casting, continuous wire casting, continuous strip casting between rolls, continuous strip casting between caterpillars, which may include devices such as a mold (or "mold") ), a liquid metal supply device (or "nozzle") a cooling system, these various furnaces, tanks and solidification devices being interconnected by channels called "chutes" in which the liquid metal can be transported.

De manière surprenante, les présents inventeurs ont constaté que, mise en contact avec un gaz asséché comprenant au moins environ 2 % en volume d'oxygène et dont la pression partielle en eau est inférieure à environ 150 Pa, une surface d'aluminium liquide s'oxyde peu ce qui permet de réaliser des coulées exemptes de défauts de surface rédhibitoires. Ce résultat est surprenant car il est communément admis qu'au contraire l'humidité contenue dans l'air permet de limiter l'oxydation des alliages d'aluminium à l'état liquide.
Dans un premier mode de réalisation de l'invention, cet effet surprenant est mis en oeuvre dans un procédé de coulée.
Le procédé selon l'invention est utile pour des alliages d'aluminium très oxydables, contenant au moins environ 0,1% de Mg et/ou au moins environ 0,1% de Li. Le procédé selon l'invention est particulièrement utile pour les alliages des familles 2XXX, 3XXX, 5XXX, 6XXX, 7XXX ou 8XXX, notamment quand ces alliages ne contiennent pas d'addition volontaire de béryllium et/ou de calcium. Le procédé selon l'invention est particulièrement avantageux pour les alliages contenant moins de 3 ppm de béryllium ou même moins de 1 ppm de béryllium et/ou moins de 15 ppm de calcium ou même moins de 5 ppm de calcium. Des exemples d'alliages pour lesquels le procédé selon l'invention est particulièrement avantageux sont, dans la famille des alliages 2XXX, les alliages AA2014, AA2017, AA2024, AA2024A, AA2027, AA2139, AA2050, AA2195, AA2196, AA2098, AA2198, AA2214, AA2219, AA2524 dans la famille des alliages 3XXX les alliages AA3003, AA3005, AA3104, AA3915 dans la famille des alliages 5XXX les alliages AA5019, AA5052, AA5083, AA5086, AA5154, AA5182, AA5186, AA5383, AA5754, AA5911 et dans_ la famille des alliages 7XXX les alliages AA7010, AA7020, AA7040, AA7140, AA7050, AA7055, AA7056, AA7075, AA7449, AA7450, AA7475, AA7081, AA7085, AA7910, AA7975.
Le gaz asséché doit contenir au moins environ 2 % en volume d'oxygène et avoir une pression partielle en eau inférieure à environ 150 Pa, préférentiellement inférieure à 100 Pa et de manière encore plus préférée inférieure à 70 Pa. Dans un mode de réalisation de l'invention particulièrement avantageux, la pression partielle en eau est même inférieure à 30 Pa, préférentiellement inférieure à 5 Pa et de manière encore plus préférée inférieure à 1 Pa . La pression partielle en eau d'un gaz est également connue sous le nom de pression de vapeur. La pression partielle d'un gaz parfait i dans un mélange de gaz parfaits de pression totale P est définie comme la pression qui serait exercée par les molécules du gaz i si ce gaz occupait seul tout le volume offert au mélange. Le point de rosée d'un gaz est la température à laquelle, tout en gardant inchangées les conditions barométriques courantes, le gaz devient saturé de vapeur d'eau. Il peut aussi être défini comme la température à laquelle la pression de vapeur serait égale à la pression de vapeur saturante. Une pression partielle en eau de 150 Pa correspond à un point de rosée de -17,9 °C et à une quantité d'eau de 0,0013 kg/m3 à cette température. Une pression partielle en eau de 100 Pa correspond à un point de rosée de -22,6 °C et à une quantité d'eau de 0,0009 kg/m3 à cette température. Une pression partielle en eau de 70 Pa correspond à un point de rosée de -26,5 °C et à une quantité d'eau de 0,0006 kg/m3 à cette température.
Le gaz asséché comprend également de manière avantageuse au moins un gaz choisi parmi air, hélium, argon, azote, dioxyde de carbone, monoxyde de carbone, produits de combustion du gaz naturel, méthane, éthane, propane, gaz naturel, composés fluorés organiques, composés chlorés organiques. L'ajout de dioxyde de carbone au gaz asséché peut dans certains cas améliorer l'effet anti-oxydant. Dans un mode de réalisation de l'invention, le gaz asséché comprend entre 1 et 10 % en volume de CO2 Cependant, cet effet étant limité et cet addition ayant un coût, la teneur en CO2 du gaz asséché est inférieure à 1% en volume ou même inférieure à 0,1 % en volume dans un autre mode de réalisation avantageux de l'invention. Dans un mode de réalisation avantageux de l'invention ledit gaz asséché est essentiellement de l'air asséché par tout moyen approprié pour atteindre la pression partielle en eau souhaitée.
Selon l'invention le gaz asséché est mis en contact avec une surface liquide d'alliage d'aluminium pendant l'essentiel de la solidification dudit alliage. La mise en contact du gaz avec la surface est de préférence réalisée de façon à établir au dessus de cette surface une atmosphère dont la teneur en eau est sensiblement égale, généralement différente de moins de 10% ou 20%, à celle du gaz asséché, c'est-à-dire de façon à éviter une diffusion significative de vapeur d'eau provenant de l'air ambiant dans ladite atmosphère.
Ainsi, quand la mise en contact est réalisée à l'aide d'un flux de gaz asséché, il est avantageux que ce flux soit suffisant par rapport à la surface liquide soumise au flux asséché de façon à établir ladite atmosphère, si ce flux est trop faible, la composition de ladite atmosphère peut être trop influencée par l'atmosphère extérieure et sa teneur en eau peut ne plus correspondre à la teneur souhaitée.
Par ailleurs, il n'est en général pas nécessaire de mettre en contact avec le gaz asséché la totalité de la surface liquide de alliage d'aluminium disponible, telle qu'illustrée par la figure 1 (14, 15), pour atteindre l'effet avantageux sur la qualité de surface des produits coulés. De manière avantageuse, la surface liquide de l'alliage d'aluminium mise en contact avec le gaz asséché représente au moins 10%, préférentiellement au moins 25 % et de manière encore plus préférée au moins 50% de la totalité de la surface liquide dudit alliage d'aluminium.
Surprisingly, the present inventors have found that, when brought into contact with a dry gas comprising at least approximately 2% by volume of oxygen and whose water partial pressure is less than approximately 150 Pa, a surface of liquid aluminum s oxidizes little, which makes it possible to make castings free from unacceptable surface defects. This result is surprising because it is commonly accepted that, on the contrary, the humidity contained in the air makes it possible to limit the oxidation of aluminum alloys in the liquid state.
In a first embodiment of the invention, this surprising effect is implemented in a casting process.
The method according to the invention is useful for highly oxidizable aluminum alloys, containing at least approximately 0.1% of Mg and/or at least approximately 0.1% of Li. The method according to the invention is particularly useful for alloys of families 2XXX, 3XXX, 5XXX, 6XXX, 7XXX or 8XXX, in particular when these alloys do not contain any deliberate addition of beryllium and/or calcium. The process according to the invention is particularly advantageous for alloys containing less than 3 ppm of beryllium or even less than 1 ppm of beryllium and/or less than 15 ppm of calcium or even less than 5 ppm of calcium. Examples of alloys for which the process according to the invention is particularly advantageous are, in the family of 2XXX alloys, the alloys AA2014, AA2017, AA2024, AA2024A, AA2027, AA2139, AA2050, AA2195, AA2196, AA2098, AA2198, AA2214 , AA2219, AA2524 in the 3XXX alloy family AA3003, AA3005, AA3104, AA3915 alloys in the 5XXX alloy family 7XXX alloys AA7010, AA7020, AA7040, AA7140, AA7050, AA7055, AA7056, AA7075, AA7449, AA7450, AA7475, AA7081, AA7085, AA7910, AA7975.
The dried gas must contain at least about 2% by volume of oxygen and have a water partial pressure of less than about 150 Pa, preferably less than 100 Pa and even more preferably less than 70 Pa. particularly advantageous invention, the partial water pressure is even less than 30 Pa, preferably less than 5 Pa and even more preferably less than 1 Pa. The water partial pressure of a gas is also known as the vapor pressure. The partial pressure of an ideal gas i in a mixture of ideal gases of total pressure P is defined as the pressure which would be exerted by the molecules of gas i if this gas alone occupied all the volume offered to the mixture. The dew point of a gas is the temperature at which, while keeping current barometric conditions unchanged, the gas becomes saturated with water vapour. It can also be defined as the temperature at which the vapor pressure would be equal to the saturation vapor pressure. A water partial pressure of 150 Pa corresponds to a dew point of -17.9°C and a quantity of water of 0.0013 kg/m 3 at this temperature. A water partial pressure of 100 Pa corresponds to a dew point of -22.6°C and a quantity of water of 0.0009 kg/m 3 at this temperature. A water partial pressure of 70 Pa corresponds to a dew point of -26.5°C and a quantity of water of 0.0006 kg/m 3 at this temperature.
The dried gas also advantageously comprises at least one gas selected from air, helium, argon, nitrogen, carbon dioxide, carbon monoxide, natural gas combustion products, methane, ethane, propane, natural gas, organic fluorinated compounds, organic chlorine compounds. Adding carbon dioxide to the dry gas can in some cases enhance the antioxidant effect. In one embodiment of the invention, the dry gas comprises between 1 and 10% by volume of CO 2 However, this effect being limited and this addition having a cost, the CO 2 content of the dry gas is less than 1% by volume or even less than 0.1% by volume in another advantageous embodiment of the invention. In an advantageous embodiment of the invention said dried gas is essentially air dried by any appropriate means to reach the desired water partial pressure.
According to the invention, the dried gas is brought into contact with a liquid surface of an aluminum alloy during most of the solidification of said alloy. The bringing into contact of the gas with the surface is preferably carried out in such a way as to establish above this surface an atmosphere whose water content is substantially equal, generally different by less than 10% or 20%, to that of the dry gas, that is to say so as to avoid a significant diffusion of water vapor from the ambient air into said atmosphere.
Thus, when the contacting is carried out using a flow of dry gas, it is advantageous for this flow to be sufficient with respect to the liquid surface subjected to the dry flow so as to establish said atmosphere, if this flow is too low, the composition of said atmosphere may be influenced too much by the external atmosphere and its water content may no longer correspond to the desired content.
Furthermore, it is generally not necessary to bring into contact with the dry gas the whole of the liquid surface of the aluminum alloy available, as illustrated by the figure 1 (14, 15), to achieve the advantageous effect on the surface quality of the cast products. Advantageously, the liquid surface of the aluminum alloy brought into contact with the dried gas represents at least 10%, preferably at least 25% and even more preferably at least 50% of the total liquid surface of said aluminum alloy.

Une surface liquide de l'alliage d'aluminium est maintenue en contact avec le gaz asséché pendant l'essentiel de la solidification. Ainsi, s'il n'est pas nécessaire de mettre en contact une surface liquide avec le gaz asséché dès l'introduction du métal liquide dans le métier de coulée, il est préférable de le réaliser dès l'établissement d'un régime stationnaire. Par exemple, dans le cas de la coulée semi-continue verticale par refroidissement direct, il est préférable de le réaliser au moins dès le début de descente du faux fond ou au moins dès le début de la coulée d'une zone qui ne sera pas coupée lors des opérations ultérieures. Il est possible de faire varier le débit d'un flux de gaz asséché pendant la coulée, notamment si des défauts de surface apparaissent. Ainsi, une augmentation du débit d'un flux de gaz asséché permet dans certains cas de faire disparaitre des sillons dans le produit coulé. Le contact entre la surface liquide et le gaz asséché peut éventuellement être supprimé avant la fin de la coulée, notamment quand on atteint une zone qui sera coupée lors des opérations suivantes. En général une surface liquide de l'alliage d'aluminium est maintenue en contact avec le gaz asséché pendant au moins 50% ou même au moins 90% de la solidification.A liquid surface of the aluminum alloy is kept in contact with the dry gas during most of the solidification. Thus, if it is not necessary to bring a liquid surface into contact with the dried gas as soon as the liquid metal is introduced into the casting machine, it is preferable to do so as soon as a steady state is established. For example, in the case of vertical semi-continuous casting by direct cooling, it is preferable to carry it out at least from the start of the lowering of the false bottom or at least from the start of the casting of a zone which will not be cut during subsequent operations. It is possible to vary the flow rate of a dry gas flow during casting, in particular if surface defects appear. Thus, an increase in the flow rate of a flow of dry gas makes it possible in certain cases to make furrows disappear in the cast product. The contact between the liquid surface and the dried gas can possibly be eliminated before the end of the casting, in particular when a zone is reached which will be cut off during the following operations. Generally a liquid surface of the aluminum alloy is kept in contact with the dry gas for at least 50% or even at least 90% of the solidification.

La présente invention s'applique à différents procédés de coulée et de préférence à un procédé de coulée choisi parmi la coulée semi-continue verticale par refroidissement direct, la coulée horizontale, la coulée continue de fil, la coulée continue de bandes entre cylindres, la coulée continue de bandes entre chenilles (« belt caster »).
Le procédé semi-continu de coulée verticale par refroidissement direct des alliages d'aluminium, connu de l'homme du métier notamment sous sa dénomination en langue anglaise « Direct Chill casting » ou « DC casting », est un procédé préféré dans le cadre de la présente invention. Dans ce procédé on coule dans une lingotière présentant un faux fond un alliage d'aluminium en déplaçant verticalement et de façon continue le faux fond de manière à maintenir un niveau de métal liquide sensiblement constant pendant la solidification de l'alliage, les faces solidifiées étant refroidies directement avec de l'eau. La figure 1 illustre ce procédé. Un alliage d'aluminium est alimenté par un conduit (4) dans une lingotière (3) posée sur un faux-fond (21). L'alliage d'aluminium se solidifie par refroidissement direct (5). L' alliage d'aluminium en cours de solidification (1) présente au moins une surface solide (11, 12, 13) et au moins une surface d'alliage d'aluminium à l'état liquide pouvant être recouverte d'oxydes, qui est appelée « surface liquide » dans la présente description (14, 15). Un descenseur (2) permet de faire descendre progressivement l'alliage en cours de solidification de façon à maintenir la position verticale de la surface d'aluminium liquide (14, 15) sensiblement constante.
The present invention applies to various casting processes and preferably to a casting process chosen from among vertical semi-continuous casting by direct cooling, horizontal casting, continuous casting of wire, continuous casting of strips between rolls, continuous casting of strips between caterpillars (“belt caster”).
The semi-continuous process of vertical casting by direct cooling of aluminum alloys, known to those skilled in the art in particular by its name in English "Direct Chill casting" or "DC casting", is a preferred process in the context of the present invention. In this process, an aluminum alloy is poured into an ingot mold having a false bottom by moving vertically and continuously the false bottom so as to maintain a substantially constant level of liquid metal during the solidification of the alloy, the solidified faces being cooled directly with water. The figure 1 illustrates this process. An aluminum alloy is fed through a conduit (4) into a mold (3) placed on a false bottom (21). The aluminum alloy solidifies by direct cooling (5). The solidifying aluminum alloy (1) has at least one solid surface (11, 12, 13) and at least one liquid state aluminum alloy surface which can be coated with oxides, which is called "liquid surface" in the present description (14, 15). A descender (2) makes it possible to gradually lower the alloy during solidification so as to maintain the vertical position of the liquid aluminum surface (14, 15) substantially constant.

Le procédé selon l'invention est notamment avantageux pour la coulée de plaques et de billettes par coulée semi-continue verticale par refroidissement direct. Le procédé selon l'invention est particulièrement avantageux pour la coulée de plaques de grandes dimensions, notamment de section supérieure à 0,5 m2.The method according to the invention is particularly advantageous for the casting of plates and billets by vertical semi-continuous casting by direct cooling. The process according to the invention is particularly advantageous for the casting of plates of large dimensions, in particular with a section greater than 0.5 m 2 .

Dans le cas de la coulée semi-continue verticale par refroidissement direct, le dispositif est fixé autour d'un injecteur de métal liquide de façon à introduire le gaz asséché du centre de la surface liquide vers sa périphérie et/ou de la périphérie vers le centre.In the case of semi-continuous vertical casting by direct cooling, the device is fixed around a liquid metal injector so as to introduce the dried gas from the center of the liquid surface towards its periphery and/or from the periphery towards the center.

Un dispositif pour l'approvisionnement du gaz dans le cas de la coulée semi-continue verticale par refroidissement direct est illustré par la figure 2. Le gaz asséché est approvisionné à l'aide d'un dispositif (6) fixé autour de l'injecteur de métal liquide (4) de sorte que le flux de gaz asséché (7) est orienté du coeur de ladite surface liquide vers sa périphérie et/ou de la périphérie vers le coeur dans la zone d'injection du métal liquide. Avantageusement, le dispositif d'approvisionnement de gaz peut être fixé sur un barrage retenant les oxydes (« barrage à crasse ») qui est positionné autour de la zone d'injection du métal liquide. De cette façon, on peut obtenir un effet du flux de gaz asséché plus important dans la zone où l'oxydation est probablement la plus élevée c'est-à-dire à proximité de l'injecteur de métal liquide, et dans la zone située entre le barrage à crasses et la lingotière, cette zone étant précisément celle la plus susceptible de générer des défauts de surface sur les produits coulés. Par ailleurs cette configuration permet également de limiter la dimension du dispositif.A device for the supply of gas in the case of semi-continuous vertical casting by direct cooling is illustrated by the figure 2 . The dry gas is supplied by means of a device (6) fixed around the liquid metal injector (4) so that the flow of dry gas (7) is directed from the core of said liquid surface towards its periphery and/or from the periphery towards the core in the liquid metal injection zone. Advantageously, the gas supply device can be fixed on a dam retaining the oxides (“dross dam”) which is positioned around the liquid metal injection zone. In this way, one can obtain a greater effect of the dry gas flow in the zone where the oxidation is probably the highest, that is to say near the liquid metal injector, and in the zone located between the dross barrier and the ingot mould, this zone being precisely the one most likely to generate surface defects on the cast products. Moreover, this configuration also makes it possible to limit the size of the device.

Le gaz asséché du procédé de coulée selon l'invention peut aussi être utilisé dans d'autres parties d'une installation de coulée sur une surface liquide d'alliages d'aluminium contenant au moins environ 0,1% de Mg et/ou au moins environ 0,1% de Li, afin d'en minimiser l'oxydation. Une installation de coulée comprend plusieurs autres dispositifs dans lesquels des surfaces liquides d'alliage d'aluminium sont en contact avec l'atmosphère. Ainsi le gaz asséché peut avantageusement être utilisé pour limiter l'oxydation de la surface liquide d'alliages dans un four, notamment de fusion ou de maintien, dans une cuve de traitement telles qu'une poche de filtration ou une poche de dégazage ou dans un chenal de transfert tel qu'une goulotte. Dans ces utilisations, on utilise de préférence des conditions de mise en oeuvre du gaz asséché et/ou une composition d'alliage d'aluminium semblables à celles du procédé selon l'invention, notamment concernant l'approvisionnement du gaz asséché. Avantageusement, dans le procédé selon l'invention, le gaz asséché est également utilisé dans au moins un four, notamment de fusion ou de maintien et/ou dans au moins une cuve de traitement telles qu'une poche de filtration ou une poche de dégazage et/ou dans au moins un chenal de transfert tel qu'une goulotte.
Les produits obtenus par un procédé selon l'invention et/ou par une utilisation selon l'invention peuvent optionnellement être corroyés notamment par laminage, filage et/ou forgeage, de façon à obtenir en particulier des tôles et des profilés.
L'invention permet notamment la coulée des alliages d'aluminium les plus oxydables, en particulier les alliages d'aluminium contenant du magnésium et/ou du lithium, sans utiliser d'additifs tels que le béryllium et/ou le calcium et sans utiliser de dispositif et/ou gaz couteux tout en obtenant des lingots coulés exempts de défauts de surface et de pollutions, en toute sécurité.
The dry gas from the casting process according to the invention can also be used in other parts of a casting installation on a liquid surface of aluminum alloys containing at least about 0.1% Mg and/or at least about 0.1% Li, to minimize oxidation. A casting installation includes several other devices in which liquid surfaces of aluminum alloy are in contact with the atmosphere. Thus the dried gas can advantageously be used to limit the oxidation of the liquid surface of alloys in a furnace, in particular melting or holding, in a treatment tank such as a filtration ladle or a degassing ladle or in a transfer channel such as a chute. In these uses, conditions for using the dried gas and/or an aluminum alloy composition similar to those of the process according to the invention are preferably used, in particular concerning the supply of the dried gas. Advantageously, in the method according to the invention, the dried gas is also used in at least one furnace, in particular melting or holding and/or in at least one treatment tank such as a filtration ladle or a degassing ladle and/or in at least one transfer channel such as a chute .
The products obtained by a process according to the invention and/or by a use according to the invention can optionally be wrought in particular by rolling, spinning and/or forging, so as to obtain in particular sheets and profiles.
The invention allows in particular the casting of the most oxidizable aluminum alloys, in particular aluminum alloys containing magnesium and/or lithium, without using additives such as beryllium and/or calcium and without using expensive device and/or gas while obtaining cast ingots free from surface defects and pollution, in complete safety.

ExemplesExamples Exemple 1Example 1

Dans cet exemple, on a mesuré l'oxydation du métal liquide par analyse thermogravimétrique. Dans ces essais, un creuset contenant le métal liquide est maintenu à une température contrôlée. Ce creuset contient environ 5 kg de métal, pour un diamètre de 100 mm. La taille significative de ces expériences qui permet de prendre en compte des effets macroscopiques peut expliquer des différences avec les expériences réalisées sur de très faibles quantités souvent rapportées dans l'art antérieur. La masse de l'échantillon est pesée en continu. La prise de poids est due à l'oxydation du métal liquide. Un schéma illustrant cette expérience est présenté sur la figure 4.
Le gaz asséché (7) est apporté à la surface du métal liquide (14) par un tube métallique (6) de diamètre intérieur 4 mm, disposé obliquement par rapport à cette surface. La balance (92) permet de mesurer en continu le poids du creuset (93) et de son contenu in situ dans le four (91). La distance entre l'orifice du tube métallique et la surface du métal liquide était 120 mm. L'air utilisé peut être asséché jusqu'à atteindre une pression partielle en eau inférieure à 70 Pa. Trois alliages ont été étudiés : les alliages AA7449, AA2196 et AA5182. Les conditions des différents essais sont résumées dans le tableau 1. Dans tous les essais, la teneur en béryllium et en calcium étaient semblables et inférieures à 1 ppm et 10 ppm, respectivement. Tableau 1. Conditions des essais réalisés avec la thermobalance Essais alliage Débit de gaz (1/mn) Gaz Pression partielle en eau du gaz injecté (Pa) 1 AA5182 7.9 Air sec < 70 Pa 2 AA5182 0 Air ambiant > 600 Pa 3 AA2196 7.9 Air sec < 70 Pa 4 AA2196 0 Air ambiant > 600 Pa 5 AA7449 4.1 Air sec < 70 Pa 6 AA7449 3.8 Air ambiant > 600 Pa 7 AA7449 0 Air ambiant > 600 Pa 8 AA7449 4.1 Air sec 180 Pa 9 AA7449 3.8 Air sec 600 Pa
In this example, the oxidation of the liquid metal was measured by thermogravimetric analysis. In these tests, a crucible containing the liquid metal is maintained at a controlled temperature. This crucible contains approximately 5 kg of metal, for a diameter of 100 mm. The significant size of these experiments, which makes it possible to take macroscopic effects into account, may explain the differences with the experiments carried out on very small quantities often reported in the prior art. The mass of the sample is weighed continuously. The weight gain is due to the oxidation of the liquid metal. A diagram illustrating this experiment is presented on the figure 4 .
The dried gas (7) is brought to the surface of the liquid metal (14) by a metal tube (6) with an inside diameter of 4 mm, arranged obliquely with respect to this surface. The balance (92) makes it possible to continuously measure the weight of the crucible (93) and of its contents in situ in the furnace (91). The distance between the orifice of the metal tube and the surface of the liquid metal was 120 mm. The air used can be dried until it reaches a water partial pressure of less than 70 Pa. Three alloys were studied: the AA7449, AA2196 and AA5182 alloys. The conditions of the different runs are summarized in Table 1. In all runs, beryllium and calcium content were similar and less than 1 ppm and 10 ppm, respectively. Table 1. Conditions of the tests carried out with the thermobalance Trials alloy Gas flow (1/min) Gas Water partial pressure of the injected gas (Pa) 1 AA5182 7.9 Dry air < 70Pa 2 AA5182 0 Ambiant air > 600Pa 3 AA2196 7.9 Dry air < 70Pa 4 AA2196 0 Ambiant air > 600Pa 5 AA7449 4.1 Dry air < 70Pa 6 AA7449 3.8 Ambiant air > 600Pa 7 AA7449 0 Ambiant air > 600Pa 8 AA7449 4.1 Dry air 180Pa 9 AA7449 3.8 Dry air 600Pa

Les figures 5 à 8 présentent les résultats obtenus.
La figure 5 montre les résultats obtenus avec l'alliage AA7449. Des gains de poids significativement plus faibles sont obtenus pour l'essai 5 pour lequel un flux d'air très sec a été réalisé. La mise en contact d'une surface liquide avec de l'air sec dont la pression partielle en eau est encore de 600 Pa (point de rosée de -0,2 °C, essai 9) ou même de 180 Pa (point de rosée de -15,6 °C, essai 8) ne permettent pas de limiter significativement l'oxydation. De même l'air ambiant ne permet pas de limiter l'oxydation avec ou sans flux (essais 6 et 7), ce qui exclut un effet uniquement mécanique lié à un flux de gaz.
La figure 6 montre les résultats obtenus avec l'alliage AA5182. On constate également pour cet alliage une oxydation significativement plus faible en présence d'un flux d'air très sec.
La figure 7 montre les résultats obtenus avec l'alliage AA2196. On constate à nouveau pour cet alliage une oxydation significativement plus faible en présence d'un flux d'air très sec.
La figure 8a est une photographie de la surface obtenue après l'essai dans le cas de l'essai 7 (air ambiant). On observe une oxydation très importante conduisant à des produits d'oxydation en forme caractéristique de choux fleur de teinte sombre. La figure 8b est une photographie de la surface obtenue après l'essai dans le cas de l'essai 5 (air sec). On observe une surface uniforme de teinte gris clair correspondant à un film fin d'oxyde.
The figures 5 to 8 present the results obtained.
The figure 5 shows the results obtained with the AA7449 alloy. Significantly lower weight gains are obtained for test 5 for which a very dry air flow was carried out. Bringing a liquid surface into contact with dry air whose water partial pressure is still 600 Pa (dew point of -0.2°C, test 9) or even 180 Pa (dew point -15.6°C, test 8) do not significantly limit oxidation. Likewise, the ambient air does not make it possible to limit the oxidation with or without flow (tests 6 and 7), which excludes a purely mechanical effect linked to a flow of gas.
The figure 6 shows the results obtained with the AA5182 alloy. A significantly lower oxidation in the presence of a very dry air flow is also observed for this alloy.
The figure 7 shows the results obtained with the AA2196 alloy. Again, for this alloy, significantly lower oxidation is observed in the presence of a very dry air flow.
The figure 8a is a photograph of the surface obtained after the test in the case of test 7 (ambient air). A very significant oxidation is observed, leading to oxidation products in the characteristic form of dark colored cauliflower. The figure 8b is a photograph of the surface obtained after the test in the case of test 5 (dry air). A uniform surface of light gray color corresponding to a thin oxide film is observed.

Exemple 2Example 2

Des plaques de section rectangulaire 446 mm x 2160 mm en alliage AA7449 ont été coulées verticalement à l'aide d'une installation de coulée semi-continue par refroidissement direct (DC-cast), en utilisant un affmage AlTiC. La longueur des plaques obtenues était comprise entre 900 mm et 4000 mm. La teneur en béryllium de l'alliage était inférieure à 1 ppm et la teneur en calcium était inférieure à 15 ppm. La figure 3 illustre le dispositif d'approvisionnement de gaz ayant été utilisé pour approvisionner de l'air sec lors de la coulée des plaques. Le dispositif est constitué de 4 tubes (611, 612, 621 et 622) régulièrement percés d'orifices (63) permettant d'injecter le gaz asséché (7) sur la surface liquide de l'alliage d'aluminium. Les tubes sont reliés par des raccords vissés (9) pour former un rectangle. Les tubes sont alimentés en gaz par deux de ces raccords vissés, par deux canalisations (81) et (82). La longueur L et la largeur 1 du dispositif (L = 1285 mm, 1 = 300 mm, espacement entre les orifices : 20 mm) représentent moins de environ 70% de la longueur et la largeur de la lingotière, de sorte que la surface soumise au flux de gaz asséché représente environ 50% de la totalité de la surface liquide de alliage d'aluminium (surface liquide totale : 0,96 m2, surface soumise à un flux asséché : 0,58 m2).
Le gaz asséché était de l'air sec dont la pression partielle en eau était de 60 Pa, contenant dans certains cas 5% en volume de CO2.
Plates of rectangular section 446 mm x 2160 mm in AA7449 alloy were cast vertically using a semi-continuous direct-chill casting (DC-cast) installation, using an AlTiC quench. The length of the plates obtained was between 900 mm and 4000 mm. The beryllium content of the alloy was less than 1 ppm and the calcium content was less than 15 ppm. The picture 3 illustrates the gas supply device having been used to supply dry air during the casting of the plates. The device consists of 4 tubes (611, 612, 621 and 622) regularly pierced with orifices (63) making it possible to inject the dried gas (7) onto the liquid surface of the aluminum alloy. The tubes are connected by screw connections (9) to form a rectangle. The tubes are supplied with gas by two of these screwed connections, by two pipes (81) and (82). The length L and the width 1 of the device (L = 1285 mm, 1 = 300 mm, spacing between the orifices: 20 mm) represent less than approximately 70% of the length and the width of the mold, so that the surface subjected to the flow of dry gas represents about 50% of the entire liquid surface of the aluminum alloy (total liquid surface: 0.96 m 2 , surface subjected to a dry flow: 0.58 m 2 ).
The dried gas was dry air with a water partial pressure of 60 Pa, containing in some cases 5% by volume of CO 2 .

Le tableau 2 décrit les conditions des différents essais réalisés ainsi que les résultats obtenus. Tableau 2. Condition des essais de coulée et résultats obtenus. Essai Longueur coulée [mm] flux d'air sec [m3/h] (longueur coulée) % CO2 du flux d'air sec observations 21 917 Aucun - Sillons verticaux longs (~200mm) et profonds 22 2776 Aucun (Démarrage) - Sillons verticaux longs (∼200mm) et profonds 22 (1150 mm) 5% Aucun sillon 23 3575 22 (Démarrage) 0% Quelques sillons verticaux courts (-40 mm) et peu profonds 27 (1150 mm) 0% Quelques sillons verticaux courts (-40 mm) et peu profonds 32 (2500 mm) 0% Aucun sillon Table 2 describes the conditions of the various tests carried out as well as the results obtained. Table 2. Casting test condition and results obtained. Test Cast length [mm] dry air flow [m 3 /h] (cast length) % CO2 of dry air flow comments 21 917 Any - Long (~200mm) and deep vertical furrows 22 2776 None (Startup) - Long (∼200mm) and deep vertical furrows 22 (1150mm) 5% No furrow 23 3575 22 (Start) 0% A few short (-40 mm) and shallow vertical furrows 27 (1150mm) 0% A few short (-40 mm) and shallow vertical furrows 32 (2500mm) 0% No furrow

L'effet de l'air sec a été démontré a plusieurs reprises : ainsi lors de l'essai 22, la mise en contact d'une surface liquide avec de l'air sec a permis de faire disparaitre les sillons profonds. De même dans l'essai 23, la présence d'air sec a permis dès le démarrage d'obtenir une qualité de surface satisfaisante pour les plaques coulées (quelques sillons verticaux courts (-40 mm) et peu profonds). On note de plus pour cet essai que l'augmentation du flux d'air sec a permis de faire disparaitre les sillons. L'effet de la présence de CO2 dans le gaz asséché sur la qualité de surface est, s'il existe, du deuxième ordre par rapport à l'effet de la pression partielle en eau. Ainsi pour l'essai 23, un résultat satisfaisant est obtenu en l'absence de CO2.The effect of dry air has been demonstrated on several occasions: thus during test 22, bringing a liquid surface into contact with dry air made it possible to make the deep furrows disappear. Similarly in test 23, the presence of dry air made it possible from the start to obtain a satisfactory surface quality for the cast plates (a few short (-40 mm) and shallow vertical grooves). It is further noted for this test that the increase in the flow of dry air made it possible to make the furrows disappear. The effect of the presence of CO 2 in the dry gas on the surface quality is, if it exists, of the second order compared to the effect of the partial water pressure. Thus for test 23, a satisfactory result is obtained in the absence of CO 2 .

Claims (11)

  1. Casting process for an aluminum alloy containing at least 0.1% of Mg and/or at least 0.1% of Li in which a liquid surface of said alloy is put into contact in a facility for casting with a dried gas including at least 2% of oxygen by volume and with a water partial pressure lower than 150 Pa throughout most of the solidification process in which said gas is supplied using a device (6) fixed around the molten metal injector (4) so that the dried gas flow is directed from the heart of said liquid surface towards its edge and/or from the edge towards the heart in the molten metal injection zone..
  2. Process according to claim 1 in which the water partial pressure of said dried gas is less than 100 Pa and preferably less than 70 Pa.
  3. Process according to claim 1 or claim 2 in which the gas is brought into contact with said surface in order to establish, above said surface, an atmosphere whose water content is substantially equal to that of the dried gas.
  4. Process according to any of claims 1 to 3 in which said liquid surface of aluminum alloy subjected to the dried gas flow accounts for at least 10%, and preferably at least 25% and preferably still at least 50% of the whole of the liquid surface of said aluminum alloy.
  5. Process according to any of the claims 1 to 4 in which said aluminum alloy is an alloy of the family 2XXX, 3XXX, 5XXX, 6XXX, 7XXX or 8XXX.
  6. Process according to claim 5 in which said aluminum alloy does not contain any deliberate addition of beryllium and/or calcium.
  7. Process according to any of claims 1 to 6 in which said dried gas also includes at least one gas chosen from air, helium, argon, nitrogen, carbon dioxide, carbon monoxide, natural gas combustion products, methane, ethane, propane, natural gas, organic fluorinated compounds, organic chlorinated compounds.
  8. Process according to claim 7 in which said dried gas is mainly air.
  9. Process according to any of claims 1 to 8 in which the CO2 content of dried gas is less than 1% by volume and preferably less than 0.1% by volume.
  10. Casting process according to any of claims 1 to 9 chosen from direct chill casting, horizontal casting, continuous casting of wire, continuous casting of strips between cylinders, and continuous casting of strips using a belt caster.
  11. Casting process according to any of claims 1 to 10 in which said dried gas is also used in at least one furnace, in particular a smelting or holding furnace and/or in at least one treatment tank such as a filtration ladle or a degassing ladle and/or in at least a transfer channel such as a transfer trough.
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US8479802B1 (en) * 2012-05-17 2013-07-09 Almex USA, Inc. Apparatus for casting aluminum lithium alloys
US8365808B1 (en) 2012-05-17 2013-02-05 Almex USA, Inc. Process and apparatus for minimizing the potential for explosions in the direct chill casting of aluminum lithium alloys
EP3117931B1 (en) 2013-02-04 2020-10-21 Almex USA, Inc. Apparatus for minimizing the potential for explosions in the direct chill casting aluminum lithium alloys
US9936541B2 (en) 2013-11-23 2018-04-03 Almex USA, Inc. Alloy melting and holding furnace
CN107532849B (en) 2015-02-18 2019-09-06 应达公司 Electric induction melting and holding furnace for active metal and alloy
CN109158575A (en) * 2018-09-12 2019-01-08 中国航发哈尔滨东安发动机有限公司 A kind of anti-burning method of large size magnesium alloy pouring
CN110193588B (en) * 2019-07-10 2021-01-12 东北大学 Aluminum-lithium alloy low-frequency square wave electromagnetic continuous casting device and method
CN111036869A (en) * 2019-12-30 2020-04-21 西南铝业(集团)有限责任公司 Casting process and casting system

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